Deacidification of Soybean Oil Combining Solvent Extraction and Membrane Technology

The aim of this work was to study the removal of free fatty acids (FFAs) from soybean oil, combining solvent extraction (liquid-liquid) for the separation of FFAs from the oil and membrane technology to recover the solvent through nanofiltration (NF). Degummed soybean oil containing 1.05 ± 0.10% w/w...

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Main Authors: M. L. Fornasero, R. N. Marenchino, C. L. Pagliero
Format: Article
Language:English
Published: Hindawi Limited 2013-01-01
Series:Advances in Materials Science and Engineering
Online Access:http://dx.doi.org/10.1155/2013/646343
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spelling doaj-03021df8e1854c908fedd24a30594d3f2020-11-24T20:53:51ZengHindawi LimitedAdvances in Materials Science and Engineering1687-84341687-84422013-01-01201310.1155/2013/646343646343Deacidification of Soybean Oil Combining Solvent Extraction and Membrane TechnologyM. L. Fornasero0R. N. Marenchino1C. L. Pagliero2Departamento de Tecnología Química-UNRC-CONICET-FONCyT, Ruta Nac. 36 Km 601, 5800 Río Cuarto, ArgentinaDepartamento de Tecnología Química-UNRC-CONICET-FONCyT, Ruta Nac. 36 Km 601, 5800 Río Cuarto, ArgentinaDepartamento de Tecnología Química-UNRC-CONICET-FONCyT, Ruta Nac. 36 Km 601, 5800 Río Cuarto, ArgentinaThe aim of this work was to study the removal of free fatty acids (FFAs) from soybean oil, combining solvent extraction (liquid-liquid) for the separation of FFAs from the oil and membrane technology to recover the solvent through nanofiltration (NF). Degummed soybean oil containing 1.05 ± 0.10% w/w FFAs was deacidified by extraction with ethanol. Results obtained in the experiences of FFAs extraction from oil show that the optimal operating conditions are the following: 1.8 : 1 w : w ethanol/oil ratio, 30 minutes extraction time and high speed of agitation and 30 minutes repose time after extraction at ambient temperature. As a result of these operations two phases are obtained: deacidified oil phase and ethanol phase (containing the FFAs). The oil from the first extraction is subjected to a second extraction under the same conditions, reducing the FFA concentration in oil to 0.09%. Solvent recovery from the ethanol phase is performed using nanofiltration technology with a commercially available polymeric NF membrane (NF-99-HF, Alfa Laval). From the analysis of the results we can conclude that the optimal operating conditions are pressure of 20 bar and temperature of 35°C, allowing better separation performance: permeate flux of 28.3 L/m2·h and FFA retention of 70%.http://dx.doi.org/10.1155/2013/646343
collection DOAJ
language English
format Article
sources DOAJ
author M. L. Fornasero
R. N. Marenchino
C. L. Pagliero
spellingShingle M. L. Fornasero
R. N. Marenchino
C. L. Pagliero
Deacidification of Soybean Oil Combining Solvent Extraction and Membrane Technology
Advances in Materials Science and Engineering
author_facet M. L. Fornasero
R. N. Marenchino
C. L. Pagliero
author_sort M. L. Fornasero
title Deacidification of Soybean Oil Combining Solvent Extraction and Membrane Technology
title_short Deacidification of Soybean Oil Combining Solvent Extraction and Membrane Technology
title_full Deacidification of Soybean Oil Combining Solvent Extraction and Membrane Technology
title_fullStr Deacidification of Soybean Oil Combining Solvent Extraction and Membrane Technology
title_full_unstemmed Deacidification of Soybean Oil Combining Solvent Extraction and Membrane Technology
title_sort deacidification of soybean oil combining solvent extraction and membrane technology
publisher Hindawi Limited
series Advances in Materials Science and Engineering
issn 1687-8434
1687-8442
publishDate 2013-01-01
description The aim of this work was to study the removal of free fatty acids (FFAs) from soybean oil, combining solvent extraction (liquid-liquid) for the separation of FFAs from the oil and membrane technology to recover the solvent through nanofiltration (NF). Degummed soybean oil containing 1.05 ± 0.10% w/w FFAs was deacidified by extraction with ethanol. Results obtained in the experiences of FFAs extraction from oil show that the optimal operating conditions are the following: 1.8 : 1 w : w ethanol/oil ratio, 30 minutes extraction time and high speed of agitation and 30 minutes repose time after extraction at ambient temperature. As a result of these operations two phases are obtained: deacidified oil phase and ethanol phase (containing the FFAs). The oil from the first extraction is subjected to a second extraction under the same conditions, reducing the FFA concentration in oil to 0.09%. Solvent recovery from the ethanol phase is performed using nanofiltration technology with a commercially available polymeric NF membrane (NF-99-HF, Alfa Laval). From the analysis of the results we can conclude that the optimal operating conditions are pressure of 20 bar and temperature of 35°C, allowing better separation performance: permeate flux of 28.3 L/m2·h and FFA retention of 70%.
url http://dx.doi.org/10.1155/2013/646343
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